Filter Cloth for Lithium Mining: Spodumene, Lepidolite and Tailings
On the mine side of the lithium chain, the streams that reach a filter are concentrate and tailings — not battery-grade salts. This page covers that duty, and it starts by asking which machine you run, because lithium plants do not all run the same one.
What reaches the filter on a hard-rock lithium plant
Lithium comes from two quite different routes. One is brine, where lithium is recovered from solution in evaporation ponds and a chemical plant. The other is hard rock: a pegmatite ore is crushed, ground and upgraded — typically by dense-medium separation, flotation, or both — into a mineral concentrate, leaving a tailings stream behind. This page is about the hard-rock route. Brine operations are a separate circuit and nothing here transfers to them unexamined.
On that hard-rock plant there are two slurries worth filtering, and they are different slurries. The concentrate is the product: water in it is water you pay to ship, so it is dewatered to a handling and transport moisture. The tailings are the volume: they are dewatered to recover process water and to make the residue stackable or easier to place. Same plant, same ore, two duties.
Where a filter cloth is involved, it is a consumable. On a belt machine it is an endless belt built to your machine's width and circumference; on a tower press it is a single indexing cloth. Either way it is replaced on a cycle set by your duty, not by a catalogue.
Lithium carbonate and hydroxide filtration in a chemical plant is a different duty with different chemistry, different temperatures and different machines. Do not read a concentrate belt specification across to a salt plant.
Lithium salt filtration — the refinery side →Which machine are you actually running?
Lithium mining is not a one-machine industry, and that is the honest counter to this whole page. Concentrate and tailings are dewatered on rubber-belt vacuum filters in some plants, on vertical tower pressure filters in others, on indexing vacuum filters in others again, and on centrifuges where no filter medium is involved at all. There is no single “lithium cloth”, and anyone who offers you one has skipped this question.
| Machine family | How the cloth appears on it | What that means for your enquiry |
|---|---|---|
| Rubber-belt horizontal vacuum belt filter | Endless belt, clipper / PAD, edge seal | This is the machine the rest of this page is written for. |
| Vertical tower pressure filter | Endless zigzag, low elongation | A different cloth form on a batch pressure cycle. Same duty, different consumable. |
| Indexing / pan vacuum filter | Cloth indexed in steps rather than run continuously | Different cloth mechanics. We do not map these to a belt specification. |
| Solid-bowl (decanter) centrifuge | None — separation is by sedimentation in a rotating bowl | There is no filter medium to replace. Nothing on this page applies. |
The cloth moves in steps rather than running continuously, and the media logic that follows from that is its own subject. We keep these out of our belt compatibility table on purpose — listing them there would tell you a belt fits a machine it does not fit.
- BHS BF — Pharma, food, sieves. Different cloth mechanics — not mapped to our belt range.
- Metso Larox RT / Pannevis — Chemicals. Indexing vacuum — do not mix with Larox PF or RB.
If you are on a tower press rather than a belt, the cloth family is different and so is the data we need: vertical pressure filter cloth →
Process flow across a belt machine
- 01 Slurry Feed Concentrate or tailings slurry, usually thickened first, is distributed onto the moving cloth.
- 02 Filtration Vacuum pulls process water through the cloth and the cake builds on the surface.
- 03 Washing Wash stages displace entrained process water and the reagent residues it carries.
- 04 Dewatering A dry-vacuum zone pulls the cake down towards a moisture the downstream handling can take.
- 05 Cake Discharge Cake releases at the discharge roller; the cloth is washed and returns to the feed end.
Operating values for each stage — slurry temperature, pH, particle size, solids, target cake moisture — are plant-specific. We do not publish typical figures for them; they go on the confirmation list below instead.
What makes this duty hard on a cloth
Two things separate a lithium mining duty from the gypsum duties this site also covers: the feed is an abrasive silicate rather than a soft precipitate, and it arrives carrying flotation chemistry rather than acid or scrubber liquor. Both of those land on the cloth.
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An abrasive silicate feed
Hard-rock lithium ore is a silicate ore — quartz and feldspar gangue alongside the lithium mineral — and both the concentrate and the tailings carry that abrasiveness onto the cloth and onto the machine.
Cloth implication: Yarn type and weave decide how the fabric wears, but an abrasive duty also puts the machine condition on the table: a worn transporter chews belts regardless of what they are woven from.
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Flotation reagents travel with the solids
Collectors and frothers do not stop at the flotation cells. Residues arrive at the filter on the particle surfaces and in the entrained water, and they change how the cake and the fabric behave.
Cloth implication: Surface finish and cloth-wash effectiveness matter more here than on a clean inorganic duty, because organic residues are what turn a recoverable blinding into a permanent one.
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Platy and micaceous particles blind fabrics
Mica-family minerals are platy. Platy particles align flat as the cake forms, which gives a compressible, low-permeability cake and drives fines into the fabric openings.
Cloth implication: This is the single reason a lepidolite-bearing stream should not be assumed to behave like a spodumene concentrate. The weave has to be chosen against the actual particle shape and size.
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Concentrate and tailings are not one specification
The two streams come off the same plant but they are not the same slurry: different particle size distribution, different solids, different tonnage, and often a different target moisture.
Cloth implication: One belt specification covering both is an assumption, not a saving. If you run filters on both streams, tell us both duties.
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Tracking, seams and edges on a wide belt
The belt wanders on the grooved rubber transporter, touches the edge guides, and the vacuum seal starts leaking; or the joint opens and the cake wets back as it crosses the box.
Cloth implication: Fabricated length, seam squareness and edge treatment are specification decisions, not shop defaults — and on a wide mining-duty machine they decide belt life as much as the polymer does.
These are the difficulties this duty is known for at an industry level. How severe each one is on your circuit depends on numbers we do not have yet — which is what the confirmation list is for.
Belt filter families observed in lithium and mining service
These are the rubber-belt families whose published duty listings name lithium or spodumene. The evidence level is stated as we found it and not upgraded; a brand appearing here means the machine family is observed in this service, not that we have a fit record on it.
| OEM family | Industries observed | Evidence level | Next step |
|---|---|---|---|
| HASLER Filtres Philippe | Fertilizer, hydromet, Li listed | OBSERVED | Send brand + model |
| GKD HVBF equipment | Mining, Li / PGM, fertilizer | OBSERVED | Send brand + model |
| Jord HVBF / Viper | AU iron, Li tailings | OBSERVED paper | Send brand + model |
| Roytec VBF | Mining, spodumene mention | OBSERVED | Send brand + model |
| Toncin DU | CN FGD, mining, Li | Company-reported | Send brand + model |
No verified fit record yet for this machine family on our cloth. Send your dimensions to start one.
All OEM names are used for compatibility reference only.
Spodumene concentrate
Spodumene is a lithium aluminium silicate and the main hard-rock lithium mineral. A spodumene concentrate is what a pegmatite plant ships: the ore upgraded by dense-medium separation and flotation, then dewatered before it leaves site.
Two features of that stream matter to a cloth. First, it is a coarse, hard, abrasive silicate — mechanical wear is a real failure path here in a way it is not on a soft precipitate duty. Second, it has been through a flotation circuit, so reagent residues are on the particle surfaces and in the entrained water; the wash and cloth-wash stages have to cope with that and not just with solids.
Moisture on a concentrate is not a free variable either. It is shipped tonnage, and it may be written into an offtake specification, so the target the filter has to hit comes from a contract rather than from the filter's own comfort zone. That target belongs on the enquiry, because it changes which weave is worth proposing.
We have it named here because it is a real, distinct duty an engineer will search for — not because we have sized it, scored it, or hold any view on how big it is. Nothing on this page should be read as a market statement about spodumene concentrate.
Lepidolite
Lepidolite is a lithium-bearing mica, and it is processed as a lithium source in its own right as well as turning up alongside rare-earth and other pegmatite minerals. Because it is a mica, it is platy — and that changes filtration behaviour before any other variable does.
Platy particles lie flat as the cake builds. That gives a cake which is more compressible and less permeable than an equivalent mass of blocky particles, so vacuum does less work than the tonnage would suggest, wash water is more inclined to channel, and the fines that do reach the fabric are well shaped to sit in its openings. A weave chosen against a spodumene concentrate is not automatically the right weave for a lepidolite-bearing stream.
The public evidence we work from records a single observed instance of lepidolite on a horizontal vacuum belt filter, with low confidence attached to it. That is enough to say the combination exists and to take an enquiry seriously. It is not enough to claim this is an established duty, and it is not the basis for a specification. If you run it, your plant data outranks anything published.
How the cloth is specified for this duty
Selection runs backwards from the slurry. The chemistry and temperature of the liquor narrow the polymer; the particle size distribution, the particle shape and the wash requirement narrow the weave and the surface finish; the machine narrows the fabricated dimensions, the seam and the edge treatment. The candidate polymers for horizontal vacuum belt duty are PET monofilament, PET mono/multifilament combinations, polypropylene, double- and multi-layer weave constructions, and hydrolysis- or alkali-resistant specialities.
The polymer question has a real answer on this duty and it depends on one number we do not have: your liquor pH and temperature together. Polyester is hydrolysed by hot alkaline conditions — the ester bonds in the chain are attacked, and the fabric loses strength from the inside while still looking serviceable. Polypropylene stands up to alkali considerably better but has a lower continuous temperature ceiling. A flotation circuit's pH is set by its reagent scheme, not by the filter, so the liquor arriving at the belt may be well away from neutral. That is public polymer chemistry, not our measurement, and it is exactly why we ask for the pH and the temperature before proposing anything.
We are not going to tell you on a web page which polymer your lithium belt should be. That decision belongs to your liquor, your mineralogy and your machine.
Specification status
Our factory specification package has not been confirmed in writing yet, so every parameter reads UNKNOWN. Each one is fixed against your machine and slurry during the engineering review, and it is stated in the quotation — not inferred from this page.
| Parameter | Value | Unit | How it is fixed |
|---|---|---|---|
| Polymer | UNKNOWN | — | Confirmed against liquor chemistry and temperature |
| Weave / construction | UNKNOWN | — | Confirmed against particle size and the wash requirement |
| Air permeability | UNKNOWN | L/dm²/min | Test method and test pressure will be stated with the value, once the mill confirms them in writing |
| Fabric weight | UNKNOWN | g/m² | Reported with the value, once confirmed in writing |
| Abrasion behaviour | UNKNOWN | — | Confirmed per yarn and finish; no published rating stands in for your duty |
| Seam type | UNKNOWN | — | Confirmed against machine and seam photo |
| Edge treatment | UNKNOWN | — | Confirmed against machine edge seal |
| Max fabricated width | UNKNOWN | mm | Confirmed against machine width |
| Continuous temperature limit | UNKNOWN | °C | Confirmed per polymer and finish |
| Chemical limit (alkali / reagent residue) | UNKNOWN | — | Confirmed per polymer and finish |
Industry reference — not our specification
| Parameter | Industry reference | Unit | Source |
|---|---|---|---|
| Cloth life reported on one rubber-belt HVBF family (industries observed: AU iron, Li tailings) | 4–8 | months | Conference paper, third-party machine (Jord HVBF / Viper) |
| Belt width commonly quoted up to | 4.5–4.8 m | — | Equipment-family observation, third-party machines |
Both rows describe other people's machines and other people's cloth. Neither is a life figure we are offering you, and neither describes what we can supply — our own width limit is on the UNKNOWN list above until the factory confirms it.
What we can build for this duty
The parameter table above reads UNKNOWN because our own values are not confirmed in writing yet, and we will not fill that table with industry averages. This section is the other half of the answer: the options this cloth is actually built from, what each one changes, and which piece of your data decides it. Nothing below is a specification — it is the shape of the decision.
Cloth form Lithium mining runs belts, centrifuges, indexing filters and pressure filters — not one machine. Which cloth form applies is the first question rather than a detail, and this page does not assume the answer.
Recommended material direction
Two variables lead here and they pull in different directions. The feed is a hard-rock silicate — quartz and feldspar gangue — so abrasion is a real failure path rather than a theoretical one. The liquor chemistry, on the other hand, is set by the flotation reagent scheme and may be well away from neutral, and that is the half nobody can infer from the outside.
This narrows the field; it does not pick. Which polymer goes on your machine is settled against your measured numbers and not on a web page — the same position the selection section above takes. What follows is the reasoning behind that position, not a departure from it.
- Polyester (PET) PET
Continuous reference up to ~150 °C — a published property of the polymer, not a value of ours
- Acid Good
- Alkali Limited
- Hydrolysis Limited
- Abrasion Excellent
Excellent abrasion resistance and dimensional stability under tension. If the reagent liquor is neutral or acidic, this is the direction.
- Polypropylene PP
Continuous reference up to ~90 °C — a published property of the polymer, not a value of ours
- Acid Excellent
- Alkali Excellent
- Hydrolysis Excellent
- Abrasion Good
The answer if the reagent scheme runs alkaline and hot, because that is where polyester loses strength from the surface inwards. Abrasion resistance is good rather than excellent, and the reference continuous temperature is the lower of the two.
- Polyamide (Nylon 6 / 6.6) PA
Continuous reference up to ~110 °C — a published property of the polymer, not a value of ours
- Acid Poor
- Alkali Good
- Hydrolysis Moderate
- Abrasion Excellent
Excellent abrasion resistance and good alkali resistance, so it is a candidate where the two leading variables coincide. Acid rules it out, and it changes dimension with absorbed moisture.
What actually decides it The reagent scheme and the measured pH — including the cleaning pH, not only the operating one. A mineralogical breakdown, if the plant has one, settles the abrasion half of the question.
Everything in this block is reasoning from published polymer behaviour applied to the chemistry described further up this page. It is a direction, not a selection — and the selection is made against your measured numbers during the engineering review, then written into the quotation. The full polymer envelope is on the materials page.
Weave options
An abrasive feed and a wide particle distribution push the structure towards strength first and rating second.
- Double layer / multi-layer Two or more interlaced fabric layers woven as one. A fine filtering face carried on a coarse structural back — high strength with fine retention, and drainage channels inside the fabric. Watch: Thicker and heavier; more expensive to weave. The usual answer on heavy belt duties.
- Twill The crossing point steps sideways each pick, giving a diagonal rib. More flexible and more permeable than plain at the same yarn count, with better cake release. Watch: Slightly less dimensionally stable than plain.
- Plain One over, one under. The most stable and the most rigid. Tight, uniform pores; lower permeability for a given yarn. Watch: Least forgiving of dimensional movement; can blind faster on fine solids.
A fine face on a coarse structural back lets the rating and the mechanical life be specified separately instead of trading one against the other in a single layer.
Yarn form. Mono-and-multi combinations are common where the feed carries everything from concentrate fines to gangue grit in the same stream.
Yarn form, weave and surface finish are settled as one decision. The four yarn forms available are monofilament, multifilament, mono + multi combination and staple / spun.
Permeability considerations
Air permeability is the figure everyone compares and the easiest one to quote meaninglessly. It is measured per ISO 9237 at a stated pressure drop — often 200 Pa — or per ASTM D737 (Frazier). A value with no stated pressure and no stated unit is not comparable to anything, including ours. The same applies to a pore or retention rating: on a woven cloth that is a nominal figure and not an absolute cut-off, because woven media do not have a single pore size and the cake quickly becomes the real filter.
Before comparing permeability figures on this duty, settle the machine. A number measured for a belt and a number measured for a pressure filter cloth are not describing the same job, whatever units they share.
How each property is measured, and what to ask any supplier for alongside the number, is set out on the testing and inspection page. Naming the method is a fact about a public standard, not a claim about our laboratory.
Joint options
The descriptions below are written from vacuum belt practice. If your flowsheet turns out to run a pressure filter or a centrifuge instead, the same constructions are judged against different things — which is why the machine is settled first.
- Clipper (metal hook) Interlocking metal hooks crimped onto both cloth ends, joined by a pintle wire. Fitted and replaced on the machine without dismantling it. The fastest change-out. Watch: The joint is a discontinuity: it leaks vacuum as it passes the box, and it is where most belt failures start. Hook material has to suit the liquor.
- PAD / welded overlap The two ends are overlapped and thermally fused. A smoother, quieter joint that seals better than a clipper and carries load more evenly. Watch: Made off the machine or with a portable press; a change-out takes longer.
- Spiral Spiral coils on each end interlaced and pinned. Flexible, drains through the joint, distributes load along the full width. Watch: Adds an open line across the belt — not appropriate where the joint must seal.
Fabricated length, seam squareness and edge treatment are specification decisions rather than shop defaults, and on a wide mining-duty machine they decide belt life as much as the fabric does.
The four constructions drawn in cross-section: how joints fail and what each one costs you.
Edge treatment
- Cut and sealed The cut edge is thermally sealed against fraying. The baseline. Adequate where the machine edge seal is in good condition.
- Folded / hemmed The selvedge is folded back and secured. Adds thickness and stiffness at the edge where the seal rubs.
- Reinforced edge band A separate band is bonded along the selvedge. For machines that chew edges — the usual answer when a belt keeps failing at the edge while its body is sound.
- Coated / sealed band A polymer band is applied to the edge. Seals the edge against vacuum bypass as well as protecting it mechanically.
- Guide strip / tracking profile A profile bonded to the underside to run in the machine guide. Only where the machine is built for it. Fitting one to a machine that is not is a common and expensive mistake.
A reinforced edge band is the usual answer where the belt keeps failing at the edge while its body is still sound. On an abrasive hard-rock duty that failure pattern is the one to watch for.
Relevant equipment
Whatever cloth form this duty turns out to need, it is decided at the loom before it is decided anywhere else: what a weaving platform can hold — pick density, tension, width — sets what the finished cloth can be asked to do. Our weaving runs on DORNIER (Germany) and Sulzer (Switzerland) platforms, machines built for technical textiles rather than for apparel.
Mining-duty cloth is wide and heavy, and holding a consistent pick density across that width is a property of the weaving platform rather than of anything done afterwards. Our own maximum width is being confirmed in writing, so it is answered against your measured dimensions rather than quoted from this page.
Model designations, working widths and installed quantities are being confirmed against the machine nameplates and are not published until they are. A weaving platform is easy to name and hard to fake, and we would rather you were able to check.
The full platform description, the eleven process stations from yarn to crate, and the nine laboratory checks: manufacturing.
Factory capability for this duty
The rows below are the part of our capability envelope that this duty touches. The last group is the one that makes the rest of it worth reading — a supplier who can do everything has told you nothing.
Machine families
- Rubber-belt horizontal vacuum belt filter Built to your spec
Core family. Endless belt with clipper, PAD or spiral joint and a finished edge.
What decides it Brand and model, measured width and developed length, a photograph of the joint.
- Vertical / tower / stacked pressure filter Built to your spec
Core family. Endless low-elongation zigzag loop.
What decides it Plate dimensions or filtration area, plus the cloth you are replacing.
- Drum, disc, leaf or chamber press Engineering review
Not our default family. We ask what machine you run before saying anything about cloth.
What decides it The machine family, confirmed first.
Cloth construction
- Plain, twill, satin, double and multi-layer weave Built to your spec
Double layer is the usual answer on heavy belt duties — a fine face on a coarse structural back.
What decides it Strength and retention requirements together.
Fabrication
- Edge: cut and sealed, hemmed, reinforced band, coated band Built to your spec
The usual answer when a belt keeps failing at the edge while its body is still sound.
What decides it Photographs of both edges and of the machine edge seal.
What we do not do
- Quoting from an industry name alone Not offered
Two plants in the same industry run different slurries through different machines. We ask which.
The full envelope, including the machine families and services we decline: what we build to order and what we will not take on. Fifteen pages on how a specification like this is built and read: the filter cloth specification guide.
How lithium duty cloths come off the machine
A failed cloth is usually three-way: something in the cloth, something in the machine, and something in the process. On an abrasive mining duty the machine's share of the blame is larger than most buyers expect, and diagnosing it as purely a cloth problem is the fastest way to buy the same failure twice.
Abrasive wear
Cloth-side and machine-side together — yarn and finish on one hand, transporter and roller condition on the other.
Diagnose this →Blinding
Process-side: fines, particle shape and reagent residue interacting with the weave choice. Reversible at first, then not.
Diagnose this →Belt tracking and wrinkling
Often machine-side (roller alignment, edge guides) before it is cloth-side.
Diagnose this →Seam / joint failure
Cloth-side and fabrication-side: seam type, squareness, and how the joint was closed on site.
Diagnose this →Cloth life on this duty is set by abrasion and blinding, and both are plant-specific. The one published figure we have is in the industry reference table above — it is someone else's machine on someone else's ore, and it is there to show the order of magnitude people report, not to be quoted back at you as a promise. We do not put a life figure on a cloth before seeing your duty.
Measuring the old cloth and photographing where it failed is the first step in telling the three causes apart. How to measure your old belt →
What we need from you to quote
This list is the engineering RFQ in plain form — what you gather here is exactly what the form asks for. The first line is the one that decides whether there is a quotation at the end of this at all.
| What to confirm | How to get it |
|---|---|
| Which machine — and which stream | Belt filter, tower press, indexing filter or centrifuge; and whether it runs concentrate, tailings, or both. This decides whether we can quote at all. |
| Machine brand and model | Copy it off the machine nameplate. “Unknown” is an acceptable answer. |
| Belt width | Measure the old cloth across the web, not the rubber transporter. |
| Belt length (circumference) | Measure the endless loop, or give us the machine centre distances. |
| Seam type in use now | Photograph the joint close up — clipper, PAD, or spiral. |
| Photos of the old cloth | Face and back, plus wherever it failed. This is the single most useful thing you can send. |
| What failed | Life, abrasion, blinding, tracking, seam leak, or cake release. Compare against the failure modes above. |
| Ore type and mineralogy | Spodumene, lepidolite, or a mixed feed — plus a particle size distribution if the plant has one. |
| Liquor temperature and pH | From the process sheet or a recent analysis. The reagent scheme sets the pH, not the filter. |
| Duty context | Throughput, number of wash stages, target cake moisture, and whether the machine has been rebuilt. |
Before you enquire
Is there one filter cloth for lithium?
No, and the reason is not marketing caution — it is that lithium plants do not run one machine. Concentrate and tailings are dewatered on rubber-belt vacuum filters, on vertical tower pressure filters, on indexing vacuum filters and on centrifuges, and those are four different consumables, one of which is not a consumable at all. Tell us the machine first. If it turns out to be one we cannot supply a cloth for, you will get that answer instead of a quotation.
Get an engineering quote for a lithium mining duty
Three steps after you submit: an engineer checks what you sent against the machine, we come back for anything missing, and you get a quotation or a sample plan.
Every belt is fabricated to your machine dimensions — we quote per RFQ. No online checkout.
Samples available — freight terms confirmed per request.
Where to go next
HVBF Filter Cloth
The cloth family a belt duty uses: weave, polymer, seam, edge and width options.
Tower Press Cloth
If your concentrate goes to a vertical pressure filter instead of a belt.
HVBF Compatibility
OEM families, what we can fit, and what we need from each machine.
Phosphogypsum Filtration
A soft precipitate on the same machine family — useful contrast to an abrasive ore duty.